|Publication number||US5122344 A|
|Application number||US 07/472,817|
|Publication date||Jun 16, 1992|
|Filing date||Jan 31, 1990|
|Priority date||Jan 31, 1990|
|Also published as||EP0513237A1, EP0513237A4, WO1991011202A1|
|Publication number||07472817, 472817, US 5122344 A, US 5122344A, US-A-5122344, US5122344 A, US5122344A|
|Inventors||John C. Schmoegner|
|Original Assignee||Mdt Corporation|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (13), Referenced by (97), Classifications (12), Legal Events (6)|
|External Links: USPTO, USPTO Assignment, Espacenet|
This invention relates to chemical vapor sterilizers. More particularly, this invention relates to methods and apparatus for the sterilization of items by vapors generated in a small sterilizer from injected liquid sterilants.
2. State of the Art
Chemical vapor sterilizers are well known. MDT Corporation of Torrance, Calif., markets such devices under the trademark "CHEMICLAVE®," for example. Sterilizers of this type are characterized by a chamber into which a prescribed quantity of liquid sterilant chemical is introduced. The liquid is heated in the chamber, thereby creating chemical vapor sterilant. Modern systems include a reservoir for holding sufficient liquid sterilant chemical for several sterilization cycles. Sterilant is delivered in liquid form from the reservoir through a transport system to the sterilizing chamber.
Dental and medical clinics, schools, research laboratories and similar facilities often require sterilization of a few items. For small loads, a sterilizer sized to fit on a tabletop or countertop is especially advantageous.
In current chemical sterilizers, the sterilant is typically injected into the sterilizing chamber at atmospheric pressure. As a result, pockets of air or much-diluted sterilant may result in less than adequate sterilization throughout the chamber. Lengthening the exposure time is generally not a satisfactory solution.
In addition, since most facilities do not wish to invest in systems to vent the sterilizer out of doors, gases and vapors containing residual chemical sterilant components may be discharged directly into the interior of a room. The possibility exists for unacceptable levels of chemical irritants, e.g. formaldehyde, to accumulate in the room over a prolonged period.
The control systems, including the valving system, of current chemical sterilizers may also provide opportunities for undetected operator errors.
The need exists for a small chemical sterilizer which consistently provides the desired sterilization within a short turnaround time, is simple to operate, and prevents or minimizes the escape of sterilant components into the atmosphere.
The chemical sterilizer of this invention has a sealable heated sterilizer chamber supported by one or more subsystems:
(a) A sterilant injection subsystem stores the sterilant, measures a predetermined volume and injects it into the sterilizer chamber.
(b) An evacuation subsystem is engaged to the sterilizer chamber to evacuate the chamber to reduce dilution of the vaporized sterilant by air, and alternatively to pump fresh air into the sterilizer chamber to purge the spent sterilant therefrom.
(c) A purge system encompasses the evacuation means of the evacuation subsystem, but also includes means to cool and condense the spent sterilant. A waste reservoir collects the condensed sterilants, gases and vapors from the sterilizer chamber and acts as a liquid-gas separator. The gases and vapors are filtered to remove residual sterilant components, and the condensate is disposed of.
(d) A control subsystem includes appropriate valving (typically four three-way solenoid valves and at least one two-way valve); interconnecting conduits, and an electronic controller with sensor means for determining temperature, pressure, door position, valve positions and the like. The evacuation means, heater and valve positions are controlled to provide an automated chemical sterilizer with highly effective sterilization, shortened cycle time, and effective containment/treatment of chemical sterilant components. The automated system results in a sterilizer with simplified operation and reduced possibilities for operational errors.
Various embodiments of the invention may be configured to provide a chemical sterilizer in which loss of sterilant activity due to dilution with air or sterilizer gases is greatly reduced. The sterilant dose may be automatically and accurately premeasured during the prior sterilization cycle. The number of required control valves is minimized.
Several features of the invention combine to reduce the discharge of chemical sterilant components to a low level, to enhance safety and meet governmental standards.
Other benefits which may be realized by incorporating the subsystems of this invention in various embodiments include the preservation of sterilant activity which would otherwise be lost by virtue of dilution by the contained atmosphere of the sterilization chamber; the reduction of variations in sterilization conditions at different locations within the sterilization chamber; a reduction in the number of control valves required for a chemical sterilization system; the capability to automatically meter a sterilant dose for a subsequent sterilization cycle during the course of a cycle in progress, thereby reducing the time required for a series of cycles; and the overall enhancement of the sterilization procedure from the standpoints of safety and reliability.
The sterilizer of this invention is particularly in a countertop version for sterilizing relatively small loads. The sterilizer has a short turnaround time, minimal variability in sterilizing conditions, and enhanced safety. Its operation is simple and largely automated.
In the drawings, which illustrate what is presently regarded as the best mode for carrying out the invention,
FIG. 1 is a schematic view of a chemical vapor sterilizer of this invention;
FIG. 2 is a graphical representation of a typical pressure curve characteristic of a typical operation of the chemical vapor sterilizer of FIG. 1;
FIG. 3 is a block diagram of the power up software routine of an electronic control subsystem which may be used with a chemical sterilizer of this invention;
FIG. 4 is a block diagram of the main loop software routine of an electronic control subsystem useful with a chemical sterilizer of this invention;
FIG. 5 is a block diagram of the warmup routine of an electronic control subsystem useful with a chemical sterilizer of this invention;
FIG. 6 is a block diagram of the evacuation routine of an electronic control subsystem useful with a chemical sterilizer of this invention;
FIG. 7 is a block diagram of the process routine of an electronic control subsystem useful with a chemical sterilizer of this invention;
FIG. 8 is a block diagram of the purge routines of an electronic control subsystem useful with a chemical sterilizer of this invention;
FIG. 9 is a block diagram of the vent routine of an electronic control subsystem useful with a chemical sterilizer of this invention;
FIG. 10 is a block diagram of the timer-counter interrupt routine of an electronic control subsystem useful with a chemical sterilizer of this invention;
FIG. 11 is a block diagram of the lamptest routine and check maintenance indicators routine of an electronic control subsystem useful with a chemical sterilizer of this invention;
FIG. 12 is a block diagram of the autozero and error routines of an electronic control subsystem useful with a chemical sterilizer of this invention;
FIG. 13 is a block diagram of the diagnostics mainline routine of an electronic control subsystem useful with a chemical sterilizer of this invention; and
FIG. 14 is a block diagram of the solenoid valve fault routine of an electronic control subsystem useful with a chemical sterilizer of this invention.
As illustrated in FIG. 1, the components of the sterilizer of this invention include sterilizer chamber 10 which has insulated walls 27 and a sealable door 28. Preferably, the door 28 is insulated to achieve approximately the same thermal resistance as the walls 27 to avoid uneven heating and condensation on the inside of door 28.
The sterilizer also includes a sterilant injection subsystem 60, an evacuation subsystem 61, a purge subsystem 62 and a control subsystem 63. The sterilizer components including the subsystems are enclosed in a tabletop or countertop cabinet for convenient use in medical, dental, scientific and other facilities. The only utility required is electrical power.
Sterilant injection subsystem 60 includes sterilant reservoir 16 for holding liquid sterilant chemical for delivery to the sterilizer chamber 10 via shot chamber 18. The reservoir has a filling port 50 by which sterilant may be transferred from container 51 through dispenser 52. The preferred filling port 50 and dispenser 52 have the construction and method of use as described and claimed in commonly assigned, copending U.S. Pat. application Ser. No. 468,770 filed Jan. 23, 1990, of John C. Schmoegner et al. titled RESERVOIR DISPENSING SYSTEM FOR CHEMICAL STERILIZER (identified as case 1568 in the internal files of applicant.) The apparatus of that application enables the filling of reservoir 16 to a liquid level 19 which provides vapor space 20 and prevents escape of vapors to the atmosphere. The entire disclosure of the aforesaid application Serial No. 468,770, is incorporated herein by reference.
Sterilant reservoir outlet conduit 11 leads to the third port of a first three-way solenoid valve 21. Valve 21 has a first port from which a first conduit 17 extends to sterilizer chamber 10.
An additional conduit 14 leads from vapor space 20 of sterilant reservoir 16 to a third port of a second three-way solenoid valve 22. A first conduit extends from a first port of valve 22 to sterilizer chamber 10.
A second conduit 12 connected to a second port of first three-way valve 21 extends to the lower portion, preferably the bottom, of shot chamber 18. Similarly, three-way valve 22 is connected to the top of shot chamber 18 by conduit 13. When valves 21 and 22 are activated to a first open position, permitting flow between the shot chamber 18 and reservoir 16, sterilant solution will flow by gravity through conduit 11, valve 21, conduit 12, shot chamber 18, conduit 13, valve 22, and into conduit 14 to equilibrate at the liquid level 19 of sterilant in reservoir 16. This "open loop" flow path ensures rapid and complete filling of shot chamber 18 and conduits 12 and 13.
The combined volume of the shot chamber 18 and conduits 12 and 13 provides the desired quantity of sterilant to be delivered to sterilizer chamber 10 in a single sterilizing cycle.
The shot chamber 18 is situated above the sterilizer chamber 10, and the sterilant reservoir 16 is situated above the shot chamber 18 to ensure rapid flow by gravity from reservoir 16 to shot chamber 18 and then to sterilizer chamber 10.
Preferably, a filter 30 is placed in conduit 11 to prevent any solids present in the reservoir contents from reaching and clogging or damaging the solenoid valves.
Following pre-evacuation of sterilizer chamber 10 by vacuum pump 47, valve 23 to the vacuum pump is closed and liquid sterilant is introduced into the sterilizer chamber 10 by simultaneously activating both valves 21 and 22 to close the flow paths from reservoir 16 and open them to flow between sterilizer chamber 10 and shot chamber 18. Liquid sterilant in conduits 12 and 13 and in shot chamber 18 flows rapidly and completely into chamber 10 by gravity, because of the open loop low pressure equalization. Valves 21 and 22 are then deactivated and shot chamber 18 and conduits 12 and 13 are refilled in preparation for the next sterilization cycle.
The evacuation subsystem 61 includes a small vacuum pump 47 having its inlet 48 connected by conduit 42 to third three-way solenoid valve 23 and its outlet 49 connected by conduit 43 to fourth three-way valve 24. The other two ports of three-way valve 23 lead via conduit 40 to sterilizer chamber 10, and via conduit 41 to the atmosphere. Filter 46 removes particulate matter from air drawn into conduit 41 during purging of the sterilizing chamber.
The other two ports of three-way valve 24 are connected via conduit 45 to sterilizer chamber 10, and via conduit 44 to waste reservoir 36. The latter is part of purge subsystem 62.
The Thomas Series 107 vacuum pump manufactured by Thomas Industries, Inc. of Sheboygan, Wis. is particularly well adapted to this invention. Vacuum pump model number 107 CA 16 is capable of quickly attaining and maintaining a vacuum of at least -7 (minus 7) pounds per square inch gauge (PSIG), which at sea level is essentially equivalent to an absolute pressure of about 400 mm Hg. Pre-evacuating the sterilizer chamber to this pressure will remove nearly one-half of the air, resulting in a shorter "fill time" for injecting the liquid sterilant into the sterilizer chamber.
For example, the fill time may be reduced from 20 minutes to about 7 minutes by use of pre-evacuation. Furthermore, the reduced air mass in the chamber permits a greater quantity of sterilant to be used. The reduced dilution by air enhances the sterilizing activity of the vaporized sterilant.
In addition to waste reservoir 36, the purge subsystem also includes conduit 33 leading from sterilized chamber 10 to solenoid valve 32 and thence to a massive aluminum cold bar 31, through cooling coil 29, and through conduit 34 to waste reservoir 36. Sterilant vapors passing to the aluminum bar 31 and cooling coil 29 are quickly cooled to approximately room temperature, condensed and delivered to the waste reservoir 36. Air and other gasses pass via conduit 35 to filter 39 where the small quantities of sterilant components such as formaldehyde and other contaminants are removed. The filtered gas is discharged to the atmosphere. A liquid level 37 is maintained in waste reservoir 36 to provide vapor space 38. Discharge through conduit 58 of condensed sterilant is controlled by conventional means, not shown, to maintain the proper liquid level 37.
Cold bar 31 is a massive aluminum bar bored for fluid flow. It acts as a passive heat sink for quickly absorbing a large part of the spent sterilant's enthalpy. For a small tabletop sterilizer, an aluminum bar of 15 to 36 cubic inches will provide the required heat capacity.
A preferred exhaust filter system for removing residual chemical components from the waste vapors is described and claimed in a commonly assigned, copending U.S. Pat. application Ser. No. 463,442, filed Jan. 11, 1990, titled EXHAUST FILTER SYSTEM FOR STERILIZERS of John C. Schmoegner et al. The entire disclosure of now U.S. Pat. No. 5,022,898, is incorporated herein by reference. This filter system includes a liquid trap filter for capturing condensed fluids, and a canister filled with a reactive or inert chemical composition which detoxifies or captures spent sterilant components of the exhaust gases.
In practice, a pressure relief valve is installed on chamber 10 or an attached conduit such as conduit 40, as required by law and good engineering practice.
In addition, a check valve may be included in conduit 45 to ensure that sterilant vapors will not pass from chamber 10 to the vacuum pump 47. Such vapors may adversely affect the materials of construction of the pump.
A control subsystem 63 includes electronic control unit 25, pressure/temperature measurement means 26, and other measurement means, not shown. It is understood that electrical and electronic control wires, not shown, connect unit 25 to the various solenoid valves 21, 22, 23, 24 and 32, vacuum pump 47, temperature and pressure measurement devices and the like. Control unit 25 controls the sequence of operations necessary to perform the desired sterilization.
FIG. 2 graphically depicts the typical sterilizer chamber gauge pressure at each step in the sterilization process, following loading of the chamber. The figure also shows the position of the various solenoid valves 21, 22, 23, 24 and 32, as well as the condition of the vacuum pump means 47, sterilizer chamber door lock (typically a solenoid type lock), and sterilizer-chamber heater 56. The latter two components are not shown in FIG. 1, but are well-known in the field of sterilizers. Typically, one or more electrical band heaters surround the cylindrical portion of the sterilizer chamber, lying between the metal wall of the chamber and the external insulation.
As already indicated, each three-way solenoid valve has three ports for flow. It is understood that the possible valve positions include:
(a) a "de-energized" position in which fluid flow may take place between the second port and the third port, and
(b) an "energized" or "open" position in which flow may take place between the first port and the second port.
While the three-way valves may also provide (c) a "totally closed" position to restrict flow in all ports, or (d) a "totally open" position in which flow is permitted in all ports, or (e) a position in which fluid flow may take place between the first port and the third port, none of these valve positions is required or used in the presently preferred embodiments of this invention. Use of valves having more than two flow positions may be detrimental by introducing the possibility for unsatisfactory sterilization or other hazard resulting from erroneous valve positioning.
The stages of a typical sterilization cycle proceeding from a "cold start" are shown in FIG. 2. The cycle is begun with all solenoid valves in the deenergized position, the door 28 lock de-energized, vacuum pump 47 off, and heater 56 off. Valves 21 and 22 are in a de-energized condition, so shot chamber 18 is already filled with sterilant. Upon turning the power on, solenoid valve 32 is opened, chamber heater 56 is energized to begin heating, and the door lock is energized to an unlocked position.
Vacuum pump 47 is also started and pumps atmospheric air through filter 46, conduits 41, 42, 43, and 45 into chamber 10. Air may leave chamber 10 through the door and/or through valve 32, which is open. Control panel indicators such as lights indicate whether there is sufficient sterilant in reservoir 16, whether liquid level 19 is too high, and whether canister filter 39 is in place.
Materials to be sterilized, typically in a tray, are then placed in chamber 10, and door 28 is closed and locked. During this period, the sterilizer chamber 10 is unpressurized, i.e. at 0 PSIG, and it is being heated to a desired vaporization temperature. The temperature selected will depend upon the particular sterilant in use, but typically is about 132° C. for common chemical sterilants largely composed of alcohols with smaller concentrations of ketones and formaldehyde.
Following closure of door 28, solenoid valves 23 and 24 are "exercised," i.e., cycled on and off several times, typically five times, to dislodge any particles such as formaldehyde deposits, in the valves and to assure operability of seals.
Solenoid valves 23 and 24 are then simultaneously activated in an evacuate step to open flow of gases, e.g. air from sterilizer chamber 10 through conduit 40, valve 23, conduit 42, vacuum pump 47, conduit 43, valve 24 and conduit 44 to waste reservoir 36. The gases are discharged from reservoir 36 through filter 39.
Two-way solenoid valve 32 is also deactivated to a closed position, and chamber 10 is evacuated to a pressure of about -5 (minus 5) to -8 (minus 8) PSIG. The chamber pressure at the end of the evacuation step is shown in FIG. 2 as -7 (minus 7) PSIG.
The "dump" or "sterilant injection" step is then begun by simultaneously activating solenoid valves 21 and 22, as previously described, to permit sterilant in shot chamber 18 and conduits 12 and 13 to flow into sterilizer chamber 10. Metal instruments in the chamber quickly absorb heat to create an additional small vacuum effect, which speeds the already rapid filling process.
Vaporization of the sterilant increases the total pressure in chamber 10. At a preset chamber pressure of 3 to 12 PSIG, typically 4 PSIG, solenoid valves 21 and 22 are deactivated to open the shot chamber 18 and associated conduits to sterilant flow from reservoir 16.
At the moment valves 21, 22 are deactivated, the higher pressure in shot chamber 18 creates backflow through filter 30 for an instant, and this backflow clears particulate matter from filter 30. The backflow vapors are quickly condensed and the pressure equalizes. As it does so, liquid sterilant refills the shot chamber and associated conduits in preparation for the next sterilization cycle.
The pressure in chamber 10 continues to rise to the vapor pressure of sterilant and air, at the extant temperature, typically 20-25 PSIG at a controlled temperature of about 132° C. The pressure is dependent upon the quantities of sterilant and residual air in the chamber, the sterilant composition, the chamber volume, and the temperature. As the temperature, and associated vapor pressure, equilibrate at the desired sterilization value, the exposure time of the materials undergoing sterilization is measured and controlled. Typically, the exposure times may be in the range of 7 to 20 minutes, depending upon the load size. The shorter exposure time is useful for sterilizing a small number of unwrapped medical or dental instruments.
Upon reaching the desired exposure time, a "vent" step is initiated. Two-way solenoid valve 32 is activated to an open position. Pressurized vapors flow from chamber 10 through bar 31 and cooling coil 29, and are cooled to nearly room temperature, i.e. 25-30° C. and condensed. The condensate is collected in waste reservoir 36 for subsequent disposal. Gases and vapors pass through filter 39 to remove traces of sterilant components. The chamber pressure falls to 0 PSIG as the spent sterilant is discharged.
When the chamber 10 attains a reduced pressure, preferably approximately atmospheric, solenoid valve 24 is activated so that the vacuum pump 47, operating since the "warm up" step, begins to pump atmospheric air from filter 46 through conduit 41, valve 23, conduit 42, pump 47, conduit 43, valve 24 and conduit 45 to the sterilizing chamber 10. The entering airstream is lower in temperature than the chamber or its contents. As it enters at the back of the chamber, it tends to drop, being heavier than the hot vapors. The air is heated by contact with the chamber walls and by mixing with the hot vapors and subsequently rises and mixes further with and dilutes the hot vapors. In a small chemical sterilizer, a seven minute continuous purge is generally adequate to reduce the chemical constituents of the chamber gases to below OSHA requirements. Without this purge, a much longer time is required to meet this standard.
Following the timed purge, valve 24 and pump 47 are deactivated to cut off the purge air and permit the chamber to equilibrate by reventing at atmospheric temperature.
In a subsequent first "hold" condition, the door lock is activated to open the door and permit the removal of sterilized items. This "hold" condition permits initiation of another sterilization cycle with a shortened "warm up" time.
In a second, optional "hold" condition, the heater 56 is also deactivated to cool the chamber.
If desired, the entire sterilizer can be deactivated to return it to the original "off" condition.
The control system may be set to automatically start and shut down the sterilizer at any desired time, so that it is energized only during working hours, for instance.
FIGS. 3 through 14 show the various software routines useful in the control subsystem of the sterilizer.
The "powerup" routine of FIG. 3 includes a cycle counter and a counter for the number of cycles which filter 39 has undergone. The system may be set to disable the sterilizer when a preset number of cycles following filter regeneration is reached. This routine also energizes the chamber door lock and sets the pressure gauge.
The MAIN LOOP routine of FIG. 4 controls the process from warmup to purge and vent, using the warmup, evacuation process, purge, vent and timer-counter routines shown in FIGS. 5-10.
The various control routines for testing, maintenance checks, error disposition, diagnostics and valve fault are shown in FIGS. 11-14.
One important aspect of this invention is that of increasing the concentration of sterilant vapor in the sterilization chamber. With pre-evacuation, the sterilizing vapor will be composed of approximately equal parts of sterilant and air, by volume, based on the sterilization at 132° C. and 25 PSIG pressure. Pre-evacuation to -4 PSIG increases the sterilant vapor concentration to about 64 percent, pre-evacuation to -7 PSIG increases the sterilant vapor concentration to about 75 percent, and pre-evacuation to -10 PSIG increases the sterilant concentration to about 85 percent.
This increased concentration effectively enhances the sterilization action, and reduces the possibility for "air pockets" remaining in the chamber, and producing inadequate exposure of the materials to be sterilized.
Evacuation to very low pressures, i.e., near a complete vacuum, is not generally practical without a very large capacity vacuum pump, because of the great increase in time required to obtain smaller increments in pressure. Furthermore, the additional increase in effectiveness becomes insignificant.
Incorporation of the vacuum pump into the system for evacuating the sterilizer chamber enables another procedural step to reduce sterilant component emissions and to simultaneously shorten the cycle time. Following the sterilization exposure period, discharge of the spent sterilant from the sterilization chamber is assisted by directing air from the vacuum pump outlet to chamber 10. The introduced air increases the pressure, increasing the flow to the condensing elements 31, 29. During this purging period, the continuous dilution of spent vapors quickly reduces their concentration to a sufficiently low level to meet current governmental, e.g. OSHA, standards.
Another feature of this sterilizer is the automatic cleaning of filter 30. This cleaning occurs once each cycle, following injection or dumping of liquid sterilant into the sterilizer chamber 10. As this occurs, the pressures in sterilizer chamber 10 and shot chamber 18 immediately equilibrate at a pressure somewhat greater than atmospheric. As a result, when three-way solenoid valves 21 and 22 are simultaneously shut to the sterilizer chamber 10 and opened to the sterilant reservoir 16, an instantaneous pulse of pressurized sterilant vapors and air will flow back through conduit 11 and filter 30, blowing any solids from the inlet, i.e. reservoir side of the filter. A similar pulse occurs in valve 22 and conduit 14, blowing liquid sterilant back into reservoir 16. This emptying of conduit 14 permits the subsequent rapid filling of the shot chamber 18. Otherwise, the liquid in conduit 14 and in reservoir 16 are at the same level, tending to trap vapor and gases in shot chamber 18, i.e., between the two liquid heads, and preventing or slowing its filling.
Use of three-way valves in the arrangement described herein minimizes the number of valves required and enables efficient interaction between the valves and other components of each subsystem.
Reference herein to details of the illustrated embodiments is not intended to limit the scope of the appended claims.
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US3086263 *||Jul 8, 1960||Apr 23, 1963||Huber Johann||Sterilizing apparatus|
|US4067691 *||Apr 16, 1976||Jan 10, 1978||Mercy Hospital And Medical Center||Sterilizing system and automatic control therefor|
|US4164538 *||Nov 11, 1977||Aug 14, 1979||American Sterilizer Company||Load conditioning control method for steam sterilization|
|US4203943 *||Nov 11, 1977||May 20, 1980||American Sterilizer Company||Method of biocidal sterilization using cyclic subatmospheric pressure conditioning|
|US4261950 *||Feb 6, 1979||Apr 14, 1981||American Sterilizer Company||Sterilizing apparatus and integrated sterilizer control|
|US4309381 *||Nov 6, 1979||Jan 5, 1982||American Sterilizer Company||Establishing and ascertaining desired air removal in steam sterilization|
|US4447394 *||Aug 1, 1983||May 8, 1984||Aktiebolaget Electrolux||Method for sterilization with formalin|
|US4447399 *||May 7, 1981||May 8, 1984||Mdt Chemical Company||Combination steam and unsaturated chemical vapor sterilizer|
|US4592896 *||Aug 22, 1983||Jun 3, 1986||Mdt Biologic Company||Combination steam and unsaturated chemical vapor sterilizer|
|US4908188 *||Apr 14, 1988||Mar 13, 1990||The Scopas Technology Company, Inc.||Gas sterilant system|
|US5008079 *||Jan 19, 1989||Apr 16, 1991||Oy Santasalo-Sohlberg Ab||Apparatus and method for sterilizing or disinfecting objects|
|DE2921915A1 *||May 30, 1979||Dec 4, 1980||Webecke & Co||Sterilisation of sensitive porous articles - by vacuum and pressure application prior to active agent admission|
|FR2544615A1 *||Title not available|
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US5213774 *||Sep 10, 1991||May 25, 1993||Deutsche Babcock Anlagen Gmbh||Mobile disinfection apparatus especially for infectious waste|
|US5270948 *||Feb 1, 1991||Dec 14, 1993||Mdt Corporation||Control means including a diagnostic operating mode for a sterilizer|
|US5308579 *||Nov 25, 1991||May 3, 1994||Micro Mega Sa||Device for distribution of the liquids for an apparatus for cleaning, disinfection and lubrication of dentistry handpieces|
|US5360594 *||Nov 15, 1993||Nov 1, 1994||Winfield Industries||Control system for medical waste disposal unit|
|US5362443 *||Dec 23, 1992||Nov 8, 1994||Nippon Metal Industry Co., Ltd.||Method and apparatus for disposal of medical waste|
|US5425925 *||Mar 18, 1994||Jun 20, 1995||Winfield Industries, Inc.||Multi-stage infectious waste treatment system|
|US5480623 *||Nov 5, 1993||Jan 2, 1996||Mdt Corporation||Non-recirculating collection system for sterilizer effluent|
|US5527507 *||May 2, 1994||Jun 18, 1996||American Sterilizer Company||Accumulator based liquid metering system and method|
|US5565634 *||Jan 11, 1996||Oct 15, 1996||Minnesota Mining And Manufacturing Company||Electronic test pack using parametric measurements for sterlizers|
|US5591398 *||Apr 7, 1995||Jan 7, 1997||Olaf Tulaszowski||Method for sterilizing bone grafts|
|US5656248 *||Jun 19, 1995||Aug 12, 1997||Winfield Industries Inc.||Multi-stage infectious waste treatment system|
|US5858304 *||Jan 14, 1997||Jan 12, 1999||Steris Corporation||Vacuum jacketed steam sterilizer|
|US6066294 *||Aug 21, 1997||May 23, 2000||Ethicon, Inc.||Multi-compartment sterilization system|
|US6224828||Sep 30, 1999||May 1, 2001||Ethicon, Inc.||Method for sterilization in a multi-compartment system|
|US6273134 *||Nov 1, 1999||Aug 14, 2001||Barnstead/Thermolyne Corporation||Sterilizer valve|
|US6279622||Feb 7, 2000||Aug 28, 2001||Ethicon, Inc.||Method and system for delivering and metering liquid sterilant|
|US6390155 *||May 1, 2001||May 21, 2002||Ethicon, Inc.||Mechanism and a method for opening a sealed container|
|US6394111 *||May 11, 1998||May 28, 2002||Ethicon, Inc.||Detection of cleanliness of a medical device during a washing process|
|US6454874||Oct 14, 1999||Sep 24, 2002||Ethicon, Inc.||Method for detecting the cleanliness of a medical device|
|US6494964||Apr 25, 2002||Dec 17, 2002||Ethicon, Inc.||Monitoring of cleaning process|
|US6516817 *||May 31, 2001||Feb 11, 2003||Ethicon Inc||Monitoring of cleaning process|
|US6516818||Apr 25, 2002||Feb 11, 2003||Ethicon Inc||Monitoring of cleaning process|
|US6528015||Jun 1, 1999||Mar 4, 2003||Ethicon, Inc.||Method for sterilizing a device in a multi-compartment sterilization system|
|US6530399||May 1, 2001||Mar 11, 2003||Ethicon, Inc.||Method for delivering liquid with a container delivery system|
|US6537491 *||Jul 26, 1999||Mar 25, 2003||Abbott Laboratories||Apparatus having sterilant monitoring system|
|US6596232||Sep 29, 2000||Jul 22, 2003||Ethicon, Inc.||Device processing apparatus and method having positive pressure with two partitions to minimize leakage|
|US6645430||Aug 30, 2000||Nov 11, 2003||Ethicon, Inc.||Method and apparatus for processing device with fluid submersion|
|US6656427||Dec 22, 2000||Dec 2, 2003||Ethicon, Inc.||Sterilization process without sterile rinse|
|US6685895||Aug 29, 2000||Feb 3, 2004||Ethicon, Inc.||Method and apparatus for processing device with reduced occlusion|
|US6977061||Mar 8, 2001||Dec 20, 2005||Ethicon Endo-Surgery, Inc.||Method and apparatus for sterilizing a lumen device|
|US7211221 *||May 26, 2000||May 1, 2007||Universidad Politecnica De Cataluna||Device and method for mass deacidification, elimination of free acidity and disinfestation of cellulosic materials|
|US7229591||May 31, 2002||Jun 12, 2007||Ethicon, Inc.||Lumen sterilization device and method|
|US7246627||Dec 20, 2002||Jul 24, 2007||Ethicon, Inc.||Monitoring of cleaning process|
|US7285254||Apr 29, 2005||Oct 23, 2007||Ethicon, Inc.||Method and apparatus for sterilizing a lumen device|
|US7294305||Apr 29, 2005||Nov 13, 2007||Ethicon, Inc.||Method and apparatus for sterilizing a lumen device|
|US7429353||Jul 21, 2005||Sep 30, 2008||American Sterilizer Company||Method and apparatus for injecting a metered quantity of a liquid into a chamber|
|US7468159||Apr 29, 2005||Dec 23, 2008||Ethicon, Inc.||Method for sterilizing a lumen device|
|US7556767||Jul 31, 2003||Jul 7, 2009||Ethicon, Inc.||Integrated washing and sterilization process|
|US7640782||Apr 27, 2007||Jan 5, 2010||American Sterilizer Company||Vaporized hydrogen peroxide probe calibration rig|
|US7700056||Aug 10, 2006||Apr 20, 2010||American Sterilizer Company||Modular decontamination system|
|US7803316||Jan 31, 2003||Sep 28, 2010||Ethicon, Inc.||Method and apparatus for processing a lumen device|
|US7803317||Jun 12, 2007||Sep 28, 2010||Kaercher Futuretech Gmbh||Method for decontaminating temperature-sensitive objects|
|US7919059||Apr 27, 2007||Apr 5, 2011||American Sterilizer Company||Vaporized hydrogen peroxide decontamination system with concentration adjustment mode|
|US8007717||Aug 14, 2007||Aug 30, 2011||American Sterilizer Company||Method and apparatus for decontaminating a region without dehumidification|
|US8017074 *||Jun 30, 2006||Sep 13, 2011||Noxilizer, Inc.||Sterilization system and device|
|US8071021||Apr 27, 2007||Dec 6, 2011||American Sterilizer Company||Hydrogen peroxide vaporizer|
|US8246905 *||Apr 2, 2008||Aug 21, 2012||Microm International Gmbh||Method for disinfecting a microtome cryostat|
|US8349272||Sep 30, 2011||Jan 8, 2013||American Sterilizer Company||Hydrogen peroxide vaporizer|
|US8808622||Jul 29, 2011||Aug 19, 2014||Noxilizer, Inc.||Sterilization system and device|
|US9180217 *||Aug 18, 2014||Nov 10, 2015||Noxilizer, Inc.||Sterilization system and device|
|US9402928||Feb 27, 2013||Aug 2, 2016||Tso3 Inc.||Hydrogen peroxide sterilization method|
|US9427485 *||Feb 28, 2013||Aug 30, 2016||Tso3 Inc.||Hydrogen peroxide sterilization method|
|US9474815||Feb 27, 2013||Oct 25, 2016||Tso3 Inc.||Sterilization method and apparatus|
|US9480763||Feb 27, 2013||Nov 1, 2016||Tso3 Inc.||Hydrogen peroxide sterilization method|
|US9480764||Feb 27, 2013||Nov 1, 2016||Tso3 Inc.||Hydrogen peroxide sterilization method|
|US9480765||Feb 28, 2013||Nov 1, 2016||Tso3 Inc.||Sterilization apparatus|
|US9511157 *||Dec 10, 2012||Dec 6, 2016||Absolute Up S.R.L.||Steam steriliser|
|US9731041||Apr 19, 2013||Aug 15, 2017||Ena Co., Ltd.||Method and apparatus for sterilization with nitrogen oxide|
|US9814795||Aug 7, 2015||Nov 14, 2017||Tso3 Inc.||Sterilization method and apparatus|
|US20010036422 *||Mar 8, 2001||Nov 1, 2001||Szu-Min Lin||Method and apparatus for sterilizing a lumen device|
|US20030026729 *||May 31, 2002||Feb 6, 2003||Wu Su-Syin S.||Lumen sterilization device and method|
|US20030147775 *||Jan 31, 2003||Aug 7, 2003||Szu-Min Lin||Method and apparatus for processing a lumen device|
|US20030164182 *||Dec 20, 2002||Sep 4, 2003||Jacobs Paul T.||Monitoring of cleaning process|
|US20040105780 *||Jul 31, 2003||Jun 3, 2004||Szu-Min Lin||Integrated washing and sterilization process|
|US20050163655 *||Dec 28, 2004||Jul 28, 2005||Szu-Min Lin||Integrated washing and sterilization process|
|US20050191208 *||Apr 29, 2005||Sep 1, 2005||Szu-Min Lin||Method and apparatus for sterilizing a lumen device|
|US20050191209 *||Apr 29, 2005||Sep 1, 2005||Szu-Min Lin||Method and apparatus for sterilizing a lumen device|
|US20060057021 *||Sep 9, 2005||Mar 16, 2006||Sawyer Melvyn L||Fixed vacuum-insulated saturated steam autoclave|
|US20060088441 *||Oct 21, 2004||Apr 27, 2006||Steris Inc.||Vaporized hydrogen peroxide concentration detector|
|US20070014686 *||Jun 30, 2006||Jan 18, 2007||Arnold Ernst V||Sterilization system and device|
|US20070020141 *||Jul 21, 2005||Jan 25, 2007||Steris Inc.||Method and apparatus for injecting a metered quantity of a liquid into a chamber|
|US20070098592 *||Nov 1, 2005||May 3, 2007||Steris Inc.||Parallel flow VHP decontamination system|
|US20070166184 *||Jan 13, 2006||Jul 19, 2007||Zimmer Technology, Inc.||Methods for cleaning and sterilizing devices|
|US20080038166 *||Aug 10, 2006||Feb 14, 2008||Steris Inc.||Modular decontamination system|
|US20080159909 *||Jun 12, 2007||Jul 3, 2008||Karcher Futuretech Gmbh||Method and apparatus for decontaminating temperature-sensitive objects|
|US20080181814 *||Apr 2, 2008||Jul 31, 2008||Microm International Gmbh||Method for disinfecting a microtome cryostat|
|US20080264140 *||Apr 27, 2007||Oct 30, 2008||Steris Inc.||Vaporized hydrogen peroxide probe calibration rig|
|US20080267818 *||Apr 27, 2007||Oct 30, 2008||Steris Inc.||Vaporized hydrogen peroxide decontamination system with concentration adjustment mode|
|US20090047174 *||Aug 14, 2007||Feb 19, 2009||American Sterilizer Company||Method and apparatus for decontaminating a region without dehumidification|
|US20090087921 *||Oct 2, 2007||Apr 2, 2009||Steris Inc.||Vaporized hydrogen peroxide concentration detector|
|US20090169426 *||Jun 12, 2007||Jul 2, 2009||Karcher Futuretech Gmbh||Method and apparatus for decontaminating temperature-sensitive objects|
|US20110076192 *||Sep 29, 2010||Mar 31, 2011||Tso3 Inc.||Sterilization method and apparatus|
|US20130236373 *||Feb 28, 2013||Sep 12, 2013||Tso3 Inc.||Hydrogen peroxide sterilization method|
|US20140334977 *||Dec 10, 2012||Nov 13, 2014||Absolute Up S.R.L.||Steam steriliser|
|US20150273095 *||Aug 18, 2014||Oct 1, 2015||Noxilizer, Inc.||Sterilization system and device|
|CN104302328A *||Apr 19, 2013||Jan 21, 2015||艾那株式会社||Sterilization method using nitrogen oxide and sterilization device|
|EP0848958A2 *||Nov 7, 1997||Jun 24, 1998||Smiths Industries Public Limited Company||Autoclaves and methods of manufacture|
|EP0848958A3 *||Nov 7, 1997||Apr 19, 2000||Smiths Industries Public Limited Company||Autoclaves and methods of manufacture|
|EP1827510B1 *||Dec 13, 2005||Oct 6, 2010||Kärcher Futuretech GmbH||Method and device for decontaminating articles, especially for detoxicating or disinfecting temperature-sensitive small military devices|
|EP1904115A2 *||Jun 16, 2006||Apr 2, 2008||American Sterilizer Company||Method and apparatus for injecting a metered quantity of a liquid into a chamber|
|EP1904115A4 *||Jun 16, 2006||Oct 29, 2008||American Sterilizer Co||Method and apparatus for injecting a metered quantity of a liquid into a chamber|
|EP2266632A1 *||Feb 6, 2001||Dec 29, 2010||Ethicon, Inc||Method and system for delivering and metering liquid sterilant|
|EP2839845A4 *||Apr 19, 2013||May 27, 2015||Ena Co Ltd||Sterilization method using nitrogen oxide and sterilization device|
|WO2006063569A2 *||Dec 13, 2005||Jun 22, 2006||Kärcher Futuretech GmbH||Method and device for decontaminating articles, especially for detoxicating or disinfecting temperature-sensitive small military devices|
|WO2006063569A3 *||Dec 13, 2005||Aug 31, 2006||Kaercher Futuretech Gmbh||Method and device for decontaminating articles, especially for detoxicating or disinfecting temperature-sensitive small military devices|
|WO2007018742A3 *||Jun 16, 2006||May 2, 2008||American Sterilizer Co||Method and apparatus for injecting a metered quantity of a liquid into a chamber|
|WO2015148722A1 *||Mar 25, 2015||Oct 1, 2015||Schlumberger Canada Limited||Apparatus and methods for manual override of hydraulic choke or valve actuators|
|U.S. Classification||422/111, 422/305, 422/298, 422/307, 422/28, 422/32|
|International Classification||A61L2/24, A61L2/20|
|Cooperative Classification||A61L2/18, A61L2/24|
|European Classification||A61L2/24, A61L2/18|
|Jan 31, 1990||AS||Assignment|
Owner name: MDT CORPORATION, A CORP. OF DE., NEW YORK
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNOR:SCHMOEGNER, JOHN C.;REEL/FRAME:005223/0534
Effective date: 19900127
|Dec 11, 1995||FPAY||Fee payment|
Year of fee payment: 4
|Nov 2, 1997||AS||Assignment|
Owner name: HARVEY ACQUISITION CO., IOWA
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:GETINGE/CASTLE, INC.;REEL/FRAME:008783/0604
Effective date: 19970331
|Jun 4, 1998||AS||Assignment|
Owner name: BARNSTEAD THERMOLYNE CORPORATION, IOWA
Free format text: MERGER;ASSIGNOR:HARVEY ACQUISITION CO.;REEL/FRAME:009267/0455
Effective date: 19980430
|Dec 6, 1999||FPAY||Fee payment|
Year of fee payment: 8
|Nov 18, 2003||FPAY||Fee payment|
Year of fee payment: 12